Effluent treatment combining solid/liquid separation and pulsed electric fields

ABSTRACT

The treatment of effluents in which a flow of the effluents is subjected to a pulsed electric field that modifies physicochemical and biologic characteristics of the medium, this modification being used during a solid/liquid separation operation, of the settlement or membrane filtration type. The solid/liquid separation operation and the application of a pulsed electric field are operations carried out at different locations along the effluent flow. The pulsed electric field has voltage value, current value, pulse repetition frequency, and voltage front shape characteristics chosen such that the required effluent treatment can be achieved as a function of the locations at which these membrane filtration operations are carried out and a pulsed electric field is applied.

TECHNICAL DOMAIN

This invention relates to a method and installation for the treatment ofeffluents using pulsed electric fields, the effect of which is aphysicochemical and biological modification of an aqueous medium, usedin membrane filtration.

Water needs in France (water for human consumption, industrial water,water for agriculture purposes) accounts for 700 m³/year and perinhabitant. Human consumption is of the order of 300 l/day and perinhabitant. Water needs for a town require treatment on the upstream anddownstream sides.

Consequently, water management is a very important activity at themoment, at three different levels:

-   -   the upstream resource,    -   water treatment before use, much of which relates to human        consumption (which can be referred to as “drinking water        treatment” for simplification purposes);    -   treatment of releases into the environment. Conventionally,        these are aqueous releases from treatment plants and residual        sludge. More broadly, this treatment includes water treatment        before reuse (or tertiary treatments), often for agricultural or        industrial purposes.

Since water is the solvent of life, natural organisms proliferate in it.Some of these are pathogenic (bacteria, yeast, parasites), or willcontain pathogenic organisms (amoeba) or will enable viruses to developin host cells.

In some cases, metabolic compounds of microorganisms may be pathogenic(toxins of cyanobacteria).

In other cases, natural chemical compounds (nitrogen derivatives) andanthropic compounds (arsenic, mercury, insecticide residues, antibioticresidues) may be the source of health problems.

These compounds have different sizes and have different compositions.Sizes may vary from a few millimetres for some parasites (Ascarislumbricoides, anguillula intestinalis), of the order of a few tens ofmicrometers for their eggs or amoeba (50 μm), a few micrometers forbacteria and fungi (0.3 μm for the smallest dimension of pseudomonadiminuta), a few nanometers for viruses (25 nm for the poliomyelitisvirus) and of the order of one nm for the smallest dissolved compounds.Microorganisms may be in sporulated form, strongly resistant to externalaggression. The pathogenicity due to biological organisms (unlikechemical compounds) occupies an important place particularly due to theafter growth aspect of most bacteria. This aspect is particularlyimportant when it concerns immunodeficient subjects, with species suchas protozoan cysts such as Cryptosporidium parvum.

In order to facilitate understanding of this document, the reader isinformed about the risk of confusion between the biomembrane of amicroorganism and the separating membrane of the filtration method. Thefirst term explicitly refers to the plasma membrane composed of a doublelipidic layer. The second term will be qualified as a “process”membrane, or a filtration membrane, or a filter membrane, or simply as“membrane/PEF coupling” without any further clarification.

STATE OF PRIOR ART

Conventional water treatments cover all flows of drinking water,wastewater and sludge derived from conventional treatments so as torespect promulgated standards.

Chronologically, the objectives are to eliminate the particulatefraction (compounds larger than one micrometer), the colloidal fraction(a few tens of nanometres), and then the soluble fraction. These stepsinvolve the following in sequence:

-   -   preliminary treatments (screening, desanding, deoiling,        sieving),    -   clarification treatments (coagulation, flocculation, flotation),    -   disinfection (chemical or physical),    -   finishing treatments (elimination of micro-pollutants by        oxidation, absorption on active carbon, nanofiltration, etc.).

The normal drinking water treatment is composed of physical treatments(screening, sand filtration, etc.), physicochemical treatments(coagulation, flocculation), completed by a finishing step, the purposeof which is to avoid after growth of macro-organisms or the eliminationof soluble organic molecules; chlorination, ozonation, oxidation byhydrogen peroxide, ultraviolet radiation, nanofiltration, adsorption onactive carbon.

One emerging trend facilitates total separative treatment (by reverseosmosis) to obtain perfectly purified water, and finally to reconstitutea food quality water by the addition of salts and trace elements. Thisis the case of “bottled water” techniques, for which the demand isgrowing strongly both in developed countries (for taste “comfort”reasons) and in developing countries (for microbiological healthreasons).

For wastewater, the essential purpose of the techniques involved is toobtain a concentration of pathogenic compounds, suspended solids andsoluble compounds compatible with the receiving medium. In practice,techniques involved enable a reduction in the chemical oxygen demand(COD) such that the residual COD is less than 80 to 100 mgL⁻¹, or areduction in the biological oxygen demand (BOD) such that the BOD₅ isless than 20 mgL⁻¹.

The most conventional techniques are aerobic biological treatments(final oxidation of dissolved compounds, for example of the glucidictype in CO₂ and H₂O form) and anaerobic biological treatments(fermentation in the absence of oxygen, for which the final stage isrelease of methane). In both cases, the technique is a method fordegradation of organic material by a bacterial biomass involvingoxidation—reduction reactions catalysed by specific enzymes.

The bacteriological quality of residual water subjected to a tertiarytreatment is normally less stringently controlled than for drinkingwater, due to the fact that this water will not be ingested directly.Nevertheless, considering that this water could be reused, the rules arebecoming stringent, like “title 22” in California (22 coliforms perlitre are tolerated in water reuseable for agriculture) and the methodsinvolved are increasingly similar to methods used for drinking watertreatment.

In the domain of sludge, 22 kilograms of dry matter are producedannually per equivalent inhabitant (which means more than a milliontonnes per year in France), derived from the treatment of residual urbanor industrial water. Originally, sludges are an extremely liquidsuspension, with a content of dry matter equal to 0.5 to 5%. This sludgemay be hydrophilic (which is usually the case) or hydrophobic, withphysical or biological origin depending on the treatment from which theyare derived.

Globally, sludge contains mineral material, organic material originatingfrom cellular catabolism, and parasite pathogenic organisms (bacteria,helminth eggs). The difficulty is to produce stabilised sludges (15 to30% dryness, non fermentable) and hygienised (the concentration ofpathogenic organisms is reduced to very low levels respecting standardsissued by the Ministry of Health, particularly for salmonella, helmintheggs and enteroviruses).

When the initial effluent contains a large quantity of colloids andsuspended solids, a physical coagulation treatment is used. Eventually,the sludge content is increased (compared with the entering material)due to the addition of coagulation additives; specific polymers,trivalent metals (Al, Fe) in the form of hydroxides or chlorides.

When the majority of the material is dissolved, biological treatment ispreferred. The treated sludges then contain biological residues but alarge proportion of the entering content is oxidised in the form ofwater and gas. The sludge quantity is usually less than the enteringcontent. On average (average or high entering content, for a residualBOD of 25 to 40 mgL⁻¹), the sludge production is ½ or ⅓ of the enteringBOD mass expressed in kg BOD₅/m³d. But this strongly depends on theglobal performances of the treatment, particularly progress with enzymeexocellular hydrolysis reactions that enable maximum possibleassimilation of compounds dissolved by enzyme endocellular reactions.

Energy consumption and additives consumption (physicochemicaltreatments) parameters are essential to evaluate the advantages and thedisadvantages of the various technologies. Furthermore, the efficiencyof the different techniques needs to be compared (for example microbialreduction) taking account of incidental risks related to the use of aparticular technique (for example failure of a chlorometre or breakageof a filtration membrane) or considering undesirable by-products(chlorinated derivatives when chlorine is used, brominated derivativesfollowing ozonation treatment in the presence of bromine; these productsare usually grouped under the term DBP “Disinfection By-Products”).

Final chlorination is the least expensive technique, but somemicroorganisms such as Cryptosporidium are resistant to this treatment.Furthermore, this treatment is only recommended at the end of thetreatment so as to avoid forming DBPs.

Ozonation raises the problem of residual elimination of this oxidant.Its action on Cryptosporidium cysts remains limited. Some DBPs may alsobe formed.

UV technologies are efficient due to the efficiency of radiation on theDNA of microorganisms, and on the RNA of viruses. The difficulty is tomake sure that the entire liquid flow actually receives a minimumradiation dose. This problem is solved if there are no short circuits inthe UV reactor. The dose is then calculated by the use of complex modelstaking account of the reactor geometry, the type of lamps, aging of thelamps, the liquid flow to be treated, and the characteristics of theliquid to be treated, particularly transmittance to radiation. Thesetreatments are often the final step after elimination of suspendedsolids (MES) and turbidity.

The advantage of filtration membranes is to collect several functionsdepending on the breakdown threshold used; elimination of suspendedsolids, microorganisms, turbidity, dissolved compounds. In terms of areduction in pathogenic organisms, membranes have best performances ifthe breakdown threshold is below micro-filtration. Nevertheless, risksof a new release of microorganisms are not strictly controlled, which isthe reason why this method is not approved by the Ministry of Health.Filtration membrane integrity tests are compulsory to guard against thistype of problems.

Unfortunately, the essential disadvantage of filtration membranes istheir sensitivity to clogging, which normally involves initialpreliminary treatments, or even several filtration steps in series withincreasingly small pore sizes.

Systems involving pulsed electric fields (PEF) have been developed on alarge scale by the development of electronic systems switching very highinstantaneous powers, and with high reliability. New electronic systemsdeveloped in France by the Commissariat à l' Energie Atomique within alaser controlled uranium enrichment program (MOS cards) enable pulsesshorter than one microsecond, with practically no frequency limitation.

The first usage domain is cold sterilisation of food. This techniqueavoids thermal degradation of food products. It is only applicable topumpable products including fruit juice concentrates, egg whites,various liquids, etc.

In terms of “mass” treatment of industrial water, the use of thistechnique is mentioned as a means for preventing biological clogging(incrustation of molluscs in pipework) in nuclear power station heatexchangers. Nuclear power stations are concerned by the treatment ofcoolant system flows following the discovery of amoeba (Naegleriafowleri, Nf) in Nogent-sur-Seine power station in France.

These industrial systems are at the other end of the scale to laboratorymicro-systems specialised in genetic manipulations that have existed forseveral decades and only treat a few millilitres.

The effects conventionally mentioned are poration effects and death ofthe cell by a “capacitor” effect due to the existence of a doubleinsulating lipidic layer at the plasma membrane. Probable effects ofmolecular resonance are also mentioned, with a direct effect on the DNAof the nucleus. Some biological functions (synthesis of adenosinetriphosphate—ATP, sodium pump) may be disturbed.

For a long time, it has been thought that it would be useful toassociate a driving force not originating from mechanical energy, tocompensate for the disadvantage of clogging of filtration membranes.This is the case for electrical energy. There are many examples ofelectrical effects associated with filtration. In general, a low directvoltage is used (less than 100 V), since methods are derived fromelectrolysis or membrane electrolysis. It may involve electrocoagulationin which the metal of electrodes (aluminium, iron) is solubilised andionically associated with colloids to improve coagulation beforefiltration.

Electrofiltration in the presence of a surfactant is described as thesuperposition of an electric field onto a transmembrane pressure. Theconcentration polarisation is reduced, increasing performances in termsof flow by a factor of 10.

Chemical effects based on the production of hydrogen peroxide startingfrom dissolved atmospheric oxygen are observed with a titanium anodecovered with RuO₂. This system, called electro-peroxidation, provides ameans for oxidising chemical compounds, colloidal particles and evenmicroorganisms. These effects would make it possible to reduceresistance to transfer at the filtration membrane/solution interface.

The technical literature mentions the case of pulsed electricfields/rotofermenter (MBR) coupling in a two-stage method. The purposein the first stage (pulsed fields) is to destroy chlorinated compounds(mineralisation of chlorine) or phenolic compounds contained in anaerosol flow, in other words mostly gaseous rather than liquid.

The phenolic compounds pass through an intermediate aggregation step bypolymerisation of the phenolic nucleus. This preliminary treatmentaccelerates the biodegradation rate and therefore the final efficiencyof the MBR. Further information about this subject is given in thearticle entitled “Pulsed power for advanced wastewater remediation” byV. M Bystritskii et al., 11^(th) International Pulsed Power conference,1997, pages 79 to 84.

Coupling between pulsed fields and filtration is described for thetreatment of treatment plant sludges. U.S. Pat. No. 6 030 538 mentionsthe possibility of reducing the water content from an initial content of50% to a final value of 10 to 15%. The system combines inductionheating, on line filtration (at a pressure of the order of 70 to 105bars) and extrusion of dry sludge through calibrated orifices. Thephenomenon described is a salt-out of intra-cellular liquid, whichcontributes to reducing the water content. Key parameters include theconcentration of flocculent, the energy of pulsed fields and hydrationof sludges. The method can be used in practice to obtain drier andbiologically inert sludge to be spread.

Methods coupling pulsed electric fields and membrane filtration areparticularly attractive for the following reasons.

The nature of the effects of pulsed fields on effluent may be biological(cell destruction), physical (increase in the size of compounds insolution) and chemical (mineralisation of chlorine).

A pulsed electric field will eventually be beneficial to subsequentfiltration, due to its effect on:

-   -   small molecules by initiating radicalar reactions for degrading        micropollutants and reducing the soluble COD,    -   the colloidal fraction of a solution, characterised by surface        charges and formed by more or less organised aggregates of        molecules, macro-molecules and cellular debris,    -   splitting of macro-molecules, encouraging enzyme exocellular        hydrolysis reactions in order to reduce the production of        sludges from biological sources,    -   the release of endoplasmic molecules with a coagulating effect        (polysaccharides),    -   the destruction or inactivation of microorganisms by splitting        of the cytoplasm or by direct action on the cellular nucleus.

PRESENTATION OF THE INVENTION

The invention was designed to provide a new method and a newinstallation for the treatment of effluents combining solid/liquidseparation and pulsed electric fields, this new method and this newinstallation being easier to implement and more efficient thantechniques according to prior art.

The method according to the invention is based on coupling ofsolid/liquid separation with pulsed electric fields.

The combination of biological, physical and chemical effects introducedby pulsed electric fields provides a means for reducing the cellpopulation, making a salt-out of substances present in the cytoplasm andhydrolysis of macromolecules. Under these conditions, and unexpectedly,the biological activity of microorganisms that were not destroyed isincreased. Biological assimilation reactions are then accelerated, whichresults in an increase in the consumption rate of dissolved pollutingsubstances. Furthermore, this increase in biological activity isaccompanied by cannibalism between microorganisms which causes a globalreduction in the biomass. Finally, the release of some endo-cellularcompounds contributes to aggregating suspended solids and facilitatessubsequent liquid/solid separation.

Therefore, the purpose of the invention is a method for the treatment ofeffluents in which a flow of the said effluents is subjected to a pulsedelectric field that has the effect of modifying physicochemical andbiologic characteristics, this modification being used during asolid/liquid separation operation, the solid/liquid separation andapplication of a pulsed electric field being operations carried out atdifferent locations in the effluent flow, characterised in that thepulsed electric field is used according to a discharge mode, in otherwords a single acting mode, and has voltage value, current value, pulserepetition frequency and voltage front shape characteristics chosen suchthat the required effluent treatment is achieved as a function of thelocations at which the operations for solid/liquid separation and theapplication of a pulsed electric field are carried out.

The pulsed electric field can also be used in a discharge and chargemode, in other words double acting.

The solid/liquid separation operation may be a membrane filtrationoperation (tangential filtration, frontal or semi-frontal filtration) ora settlement operation.

Advantageously, the said modification of physicochemical and biologicalcharacteristics enables hydrolysis of dissolved substances, aggregationof colloids, complete or partial destruction of microorganisms andsimultaneous activation of remaining microorganisms.

The method according to the invention can be applied to the treatment oftreatment plant effluents and sludges, either in an activated sludgereactor, or in a rotofermenter.

Another purpose of the invention is an effluent treatment installationincluding means for performing a solid/liquid separation on a flow ofthe said effluents, and means for applying a pulsed electric field tothe flow of the said effluents, with the effect of modifying thephysicochemical and biological characteristics exploited during thesolid/liquid separation, means for separation of the solid/liquid andmeans for application of a pulsed electric field at different locationsalong the effluent flow, characterised in that means for applying apulsed electric field are means operating according to a discharge mode,in other words a single acting mode, and with voltage value, currentvalue, pulse repetition frequency and voltage front shapecharacteristics chosen such that the required effluent treatment can beachieved as a function of the locations at which these solid/liquidseparation means are used and a pulsed electric field is applied.

Means for application of a pulsed electric field may operate equallywell in discharge mode and in charge mode, in other words they aredouble acting.

Means for submitting the effluent flow to a solid/liquid separation maybe membrane filtration means (tangential, frontal or semi-frontalfiltration) or settlement means.

Advantageously, the modification of physicochemical and biologicalcharacteristics enables the hydrolysis of dissolved substances, theaggregation of colloids, complete or partial destruction ofmicroorganisms and simultaneous activation of the remainingmicroorganisms.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention will be better understood and other advantages andspecific features will become clear after reading the followingdescription given as a non-limitative example accompanied by theattached drawings among which:

FIG. 1 is an electrical diagram of a circuit assigned to a single actingtreatment head and that can be used by this invention,.

FIG. 2 is an electrical diagram of the circuit assigned to a doubleacting treatment head and that can be used by this invention,

FIG. 3 is a diagram of an effluent treatment installation according to afirst variant of this invention,

FIG. 4 is a diagram of an effluent treatment installation according to asecond variant of this invention,

FIG. 5 is a diagram of an effluent treatment installation according to athird variant of this invention,

FIG. 6 is a diagram showing the variation with time of respiration of abiomass in the endogenous phase as a function of the increase in thenumber of pulses applied.

DETAILED DESCRIPTION OF EMBODIMENTS OF THE INVENTION

For example, the embodiments described below are applicable to asolid/liquid separation obtained by membrane.

Unlike the different electrofiltration (or electro-membrane) methodsaccording to prior art, the “high potential” electrode used in thisinvention is not inside the filter membrane or is not composed of theseparating membrane itself. This aspect simplifies application of themethod. Standard commercially available membranes may be installed in amodule without adding a conducting sheet facing them (plane or spiralmembrane) and without an internal conducting nucleus (cylindricalmembrane).

This is due to the fact that within the range in which they are used,the electric fields produce physicochemical and biological effects thathave a sufficiently long duration to be beneficial for a few seconds orfew minutes.

The amplitudes of the electric field are also much higher. In practice,the effects described in old electrofiltration methods are fairlysimilar to electrolysis phenomena in which the important parameter isgeneration of a strong electrical current at a low voltage. The numberof electrons exchanged at the cathode is preponderant rather than thevoltage that remains limited to values of a few tens or hundreds ofvolts. In the new proposed membrane/PEF method, it is important to havea high voltage (5 to 30 kV) in order to produce an intense electricfield (5 to 100 kV/cm and preferably 10 to 50 kV/cm) in order to makethe plasma membrane of the microorganisms split.

Finally, the pulse repetition frequency is also an overriding parameter:depending on the nature of molecules involved in clogging, the frequencyof pulses can be adjusted to values for which a resonance phenomenonwill deactivate the compound (or the family of compounds) in order tofacilitate their passage into the “process” membrane and reduce internalclogging phenomena, particularly due to adsorption by electrostaticcharge effects.

Finally, another important parameter is the shape of the voltage front:it is preferable to have systems in which the voltage rises almostinstantaneously, unlike sinusoidal systems or when inductance effectsare too noticeable.

The effect of wave fronts could be compared with a shock wave that coulddefinitively deactivate the nucleus of a bacteria without splitting andsalt-out of the endocellular compounds.

Judicious coupling of modulable PEF effects (voltage, current,frequency, wave front), and membrane separation effects provides a meansfor obtaining the required effluent treatment.

The value of the electrical voltage current, the shape of the wave frontand the pulse repetition frequency can be given priority as required.

A high voltage can split cells and separate salted-out internalcompounds or enable reuse of them later. It also provides a means forassuring complete destruction of microorganisms and preventing theirproliferation in the form of a biofilm on the membrane surface.

The passage of a high current (in other words a large number ofelectrons) provides a means for transferring charges to charged colloidsor compounds so as to neutralise them and then to cluster them andfinally be able to separate them easily by steric segregation usingtangential filtration membranes.

The wave front is important when bacteria or other pathogenic biologicalorganisms are to be definitively deactivated by direct action on theirnucleus and so that they can be retained on filtration membranes withoutany possible proliferation and without salt-out of metabolic compounds.

The pulse repetition frequency occurs as a result of electrokineticeffects related to the dipole moment of the plasma membrane. Whenelectrokinetic forces are greater than cohesion forces of the doublelipidic layer, this layer breaks and can cause splitting and then thedeath or microorganisms.

In all methods involving pulsed electric fields divulged in prior art,it appears that users are only concerned with the “simple discharge”effect through the treatment head, more precisely through the liquidstream to be treated. This is due to the fact that the best knowneffects consist of tending to cause cell splitting. Requiredinstantaneous powers are very high, of the order of a few hundred MW for1 μs.

Normally, passage of a charge current in the treatment head is limitedby inserting an electrical element in parallel to the treatment head,for which the impedance will be zero under continuous conditions andhigh under transient conditions such as a pure inductance. FIG. 1 is theelectrical diagram for a circuit assigned to a single acting treatmenthead. The circuit comprises a DC power supply 1 varying from 1 to 20 kVand capable of outputting a current of 2 to 50 A, a pulse switch 2capable of switching from a position a to a position b, a capacitor 3and a series inductance 4. The effluent treatment head is marked asreference 5. It comprises an inductance 6 connected in parallel. Tocharge, the switch 2 is on position a and the resistance 5 representingthe treatment head is shunted by the presence of the pure inductance 6.To discharge, the switch 2 is on position b, and the high powerswitching system consisting of the capacitor 3 and the inductance 4outputs a discharge with characteristics consisting of a voltage of 5 to50 kV and a current of 500 to 2000 A for 1 μs.

In the prospect of membrane separation coupled to PEFs, the electricaleffect could also be used beneficially during charging. For example,this may be done by choosing to pass a charge current in the treatmenthead. In this case, the treatment head is installed alone as shown inFIG. 2, which is the electrical diagram for a circuit assigned to adouble acting treatment head. The charge time is usually of the order ofseveral tens of μs, so that the resulting time necessary (colloidalaggregation) for transferring charges or transferring material can berespected. This time is longer than the transfer of electrons since thespecies (molecules, colloids) have to be renewed at the interface of theelectrodes. Charge characteristics for the treatment head are a voltageof 1 to 20 kV and a current of 2 to 50 A. During the discharge, thesecharacteristics are a voltage of 5 to 50 kV and a current of 500 to 2000A.

The advantage of passing a current in the head while charging are toprevent polarisation of the electrodes and thus extend their life, andprovide a means for transferring electrons that could aggregatecolloids, thus facilitating trans-membrane flow during the filtrationstep.

On the other hand, shunting the treatment head during the charge willimprove operating conditions at high frequency (the time between twopulses is shorter), consequently enabling the use of very steep voltagefronts.

In conclusion, the method according to the invention provides a meansfor doubling effects conventionally envisaged when using PEFs, theseeffects being used beneficially in the membrane separation step.

Passing a high current through a conducting medium is accompanied by amore of less localised and variable intensity magnetic field which coulddisturb electrical signals. This phenomenon is unexpectedly beneficialfor biological or molecular purposes. The result is deactivation ofspecific biological compounds responsible for bonding of biologicalmolecules to each other or responsible for intra-cellular bonding, andtherefore bonding of the biofilm on the filtration membrane.Furthermore, other frequency values facilitate the passage of somemolecules or ions through the filtration membrane, limiting theirchemical activity and their propensity to form complex molecules thatcould be adsorbed in-depth on the pore wall.

The potential applications of pulsed electric fields coupled withmembrane separation facilitated by the modification of physicochemicaland biological characteristics of an aqueous medium occur in allapplications for solid/liquid separation and the use of filtrationmembranes:

-   -   water treatment, reduction of the biofilm, reduction of internal        clogging, biological decontamination;    -   treatment of effluents: reduction of external clogging,        oxidation of micro-pollutants;    -   activated sludge reactors, on the input side of settlement, due        to activation of microorganisms and reduction of the biomass        quantity;    -   rotofermenters: preliminary hydrolysis step by splitting of        macromolecules before filtration;    -   hygienisation of biological sludges: destruction/splitting of        microorganisms and concentration by filtration membranes;    -   production of fruit juices: splitting of cellulose membranes        (equivalent to the plasma membrane for plants), and separation        by filtration of fibres and fragments of the vegetable cells;    -   destabilisation of water/oil suspensions or emulsions by        increase in the size of droplets in the dispersed phase and        easier separation in the two phases;    -   treatment of organic phases that are poor conductors of        electricity (compared with aqueous phases; for example,        vegetable, mineral or synthetic oils, or apolar organic        solvents).

The difference in electrical characteristics of compounds in suspensionand in solution is used to aggregate the most highly conductingcompounds and facilitate coupled filtration.

Filtration according to the invention can cover different granges:microfiltration (particle sizes between 0.1 μm and 10 μm),ultrafiltration (molecule sizes between 0.005 μm and 0.1 μm),nanofiltration (molecule sizes between 0.001 μm and 0.005 μm), reverseosmosis (molecule sizes smaller than 0.001 μm). Unlike electromembranemethods, the driving force for these filtration types is the transferpressure.

Pulsed electric fields cover the frequency range of the order of 1 Hz to100 000 Hz, preferably from 1 Hz to 10 000 Hz. The electric field canvary from 1 kV/cm to 100 kV/cm, and preferably from 3 kV/cm to 50 kV/cm.The electrical effect may be repeated between 1 and 1000 times persecond, and preferably between 1 and 100 times. Also, only part of theflow can be subjected to PEFs before filtration treatment.

Due to the fact that transformations of physicochemical and biologicalcharacteristics are long lasting, membrane/PEF coupling is done with aslight offset in time. PEFs can be applied between 0.1 and 1000 secondsbefore filtration, for example between 1 and 100 seconds. The time thatelapses between the PEF treatment and filtration is due to the residencetime t of effluents in the pipes that transport them, calculated basedon the ratio of the volume V of the installation between PEF andmembranes, and the supply flow Q to the membrane modules:t=V/Q

FIG. 3 is a diagram representing insertion of a PEF system on the inputside of filtration on the effluent supply circuit. The effluentsoriginate from a reservoir 10 and are supplied through a pipe to thetreatment installation. A pump 11 at the output from the reservoir 10pressurises the effluents and controls their circulation at a flow Q.The effluents are firstly subjected to pulsed electric fields output bya PEF device 12 before arriving at membrane systems 13, 14 and 15. Themembrane system 13 outputs a first ultrafiltrate P₁ and a retentate R₁to the membrane system 14. The membrane system 14 outputs a secondultrafiltrate P₂ and a retentate R₂ to the membrane system 15. Themembrane system 15 outputs a third ultrafiltrate P₃ and a concentrateC₁.

Coupling can also be done in the reverse order. The first step in themethod is then filtration, the second step consisting of a treatment byPEF. This is illustrated in FIG. 4, in which a PEF system is inserted onthe output side of filtration on the final ultrafiltrate (finaldisinfection) and on the concentrate (hygienisation of biologicalsludges). Effluents originate from a reservoir 20 and are suppliedthrough a pressurisation pump 21 and a circulation pump 22 arranged inseries, to a membrane system 23. The membrane system 23 outputs aultrafiltrate P₄ after passing through a PEF device 24 and a retentatethat is partially recirculated between pumps 21 and 22. The membranesystem 23 also outputs a concentrate C₂ after passage in a PEF device25. In this case, the essential objective is a final disinfectant effectafter the filtration step, so that filtration membranes for whichdisinfection has not been approved can be used (cylindrical, spiral orplane membranes). Membranes with hollow fibres can also be coupled toPEF devices. In this case, the PEF treatment is applied indifferently tothe concentrate or ultrafiltrate for hygienisation purposes.

PEF and separation treatments can also be alternated, particularly in atangential filtration loop in which the retentate conventionallycirculates several times (in other words in loop) through the “process”membrane. This is illustrated in FIG. 5. The effluents originate from areservoir 30 and are supplied through a pressurisation pump 31 and acirculation pump 32 arranged in series, to a membrane system 33. Themembrane system 33 outputs a ultrafiltrate P₅ and a retentate that ispartially put into circulation again between pumps 31 and 32 afterpassing through a PEF device 34. The membrane system 33 also outputs aconcentrate C₃.

The electrodes of the PEF device may have normal geometries—plane,concentric, etc. The required effect is that the electric field shouldhave sufficient values to deactivate the different species present andthat hydraulic pressure losses should remain within acceptable values,considering the total energy cost.

A new method for treatment of water and effluents coupling filtrationmembrane technologies and pulsed electric fields (PEF) is disclosed inthis presentation. The phenomena involved by PEFs help to modify thephysicochemical and biological characteristics and this modificationparticularly enables reduction of membrane sludge clogging throughoutthe entire range of embodiments of the method in which the driving forceis the pressure: microfiltration, ultrafiltration, nanofiltration andreverse osmosis. Due to the adjustable parameters of PEFs (intensity,voltage, frequency, wave front, etc.), these phenomena are potentially:

-   -   reduction of the biofilm (splitting and lysis or temporary        deactivation of microorganisms),    -   partial destruction of microorganisms and simultaneous        activation of the remaining microorganisms,    -   aggregation of colloids (transfer of electrical charges limiting        electrostatic repulsion),    -   preliminary hydrolysis of macromolecules (by splitting of        macromolecules),    -   oxidation of micropollutants (by formation of free radicals),    -   keeping “scale-forming” molecules in suspension.

Treatments of liquid food, drinking water, spring water, wastewater oreven water treatment plant sludge are all potential applications of thisnew method.

The advantages provided by the invention include the lack of any seriouselectrolytic effects proven by the absence of any electrode wear. Thesurface condition of electrodes after about 200 hours of operation wasstudied using a Nanofocus AG apparatus. In particular, the value of thesurface roughness confirmed that no modification had occurred duringthese 200 hours of operation. This result indicates that there was nochemical or electrochemical surface attack.

Another advantage resulting from the invention is the instantaneous andlong-lasting activation of a population of microorganisms in theendogenous phase and deactivation of a population in the presence of asubstrate. In both cases, cell mortality is due to lack of cellaftergrowth. This means that microorganisms have a metabolisationcapacity throughout their individual life. Since the microorganismsremain living, they will continue to act in two different ways. They actfirstly by excretion of metabolites facilitating solid—liquidseparation. They also act by assimilation of dissolved exogenouscompounds, causing a reduction in the effluent pollution level.

Tests were carried out in open circuit at 78 Hz (10 pulses per pass) orat 780 Hz (100 pulses per pass). The cell destruction rate wascharacterized using the numbering method on gelose. It is between 97.2and 99.2% for the test at 78 Hz and is equal to 99.97% for the test at780 Hz. A deactivation close to 4 Log is possible for energy values ofthe order of 10 kWh/m³.

Cell activity was characterised using the respirometry method.

A test was carried out in recycling mode (at 78 Hz corresponding to 10pulses per pass) in order to increase the number of treatments withtime, to determine the effect of PEFs on a yeast suspension in theendogenous phase.

FIG. 6 is a diagram showing the variation of respiration R with time asa function of the number N of applied treatments. Respiration R is givenin milligrams of oxygen per litre and per minute. The straight line 41shown in dashed lines gives the value of respiration before treatment,in other words the value of the oxygen consumption rate in theendogenous phase. The curve 42 shows the variation of respiration withtime.

It should be noted that respiration suddenly increases during the firsttreatments. The increase in respiration is of the order of 4 during thefirst 90 pulses. It reduces significantly afterwards, but it does notreturn to the initial value. The most plausible explanation is that theelectrical shock applied to the yeast causes a salt-out of endoplasmiccompounds into the medium (as proved by the increase in COD (chemicaloxygen demand) in the medium which varies from 55 mg/l to 70 mg/l).Initially, undamaged yeast reabsorbs these compounds with the effect ofincreasing respiration. Later, the number of damaged or destroyed cellsincreases causing a reduction in the total biomass activity.

Therefore the most remarkable effect is the instantaneous and suddenactivation of the biomass in the endogenous phase when it is subjectedto an electric shock. Conversely, a population in the presence of asubstrate is temporarily shocked but its metabolisation capacities arerestored throughout its life. Nevertheless, in both cases, thereproduction capacity of the biomass originates solely from the fractionthat was not shocked. There will be no aftergrowth in the shockedfraction (and fraction after lysis); this is clear whenever carrying outnumbering tests on gelose.

1-13. (canceled)
 14. A method for treatment of effluents comprising:subjecting a flow of the effluents to a pulsed electric field that hasan effect of modifying physicochemical and biologic characteristics, themodifying being used during a solid/liquid separation operation, thesolid/liquid separation and application of the pulsed electric fieldbeing operations carried out at different locations in the effluentflow, wherein the pulsed electric field is used according to a dischargemode, the discharge mode being obtained by pulse discharge of acapacitor powered by a dc power supply, and having adjustable voltagevalue, current value, pulse repetition frequency, and voltage frontshape characteristics.
 15. A method according to claim 14, wherein thepulsed electric field is used according to a charge or discharge mode,the charge mode being obtained by pulse charge of a capacitor powered bya dc power supply.
 16. A method according to claim 14, wherein thesolid/liquid separation operation comprises a membrane filtrationoperation.
 17. A method according to claim 16, wherein the membranefiltration is chosen among tangential filtration, frontal filtration,and semi-frontal type filtration.
 18. A method according to claim 14,wherein the solid/liquid separation operation comprises a settlementoperation.
 19. A method according to claim 14, wherein the pulsedelectric field has characteristics adjusted so that the modifying ofphysicochemical and biological characteristics enables hydrolysis ofdissolved substances, aggregation of colloids, complete or partialdestruction of microorganisms, and simultaneous activation of remainingmicroorganisms.
 20. Application of the method according to claim 14 totreatment of treatment plant effluents and sludge, either in anactivated sludge reactor or in a rotofermenter.
 21. An installation fortreatment of effluents, comprising: means for subjecting a flow of theeffluents to a solid/liquid separation operation; and means forsubjecting the flow of the effluents to a pulsed electric field that hasan effect of modifying physicochemical and biologic characteristics, themodifying being used during a solid/liquid separation, the means forsubjecting the flow of the effluents to the solid/liquid separationoperation and the means for subjecting the flow of the effluents to thepulsed electric field being located at different locations along theeffluent flow, wherein the means for subjecting the flow of the effluentto the pulsed electric field operates according to a discharge mode, thedischarge mode being obtained by pulse discharge of a capacitor poweredby a dc power supply, and having adjustable voltage value, currentvalue, pulse repetition frequency, and voltage front shapecharacteristics.
 22. An installation according to claim 21, wherein themeans for subjecting the flow of the effluents to the pulsed electricfield operates according to a charge and discharge mode, the charge modebeing obtained by pulse charge of a capacitor powered by a dc powersupply.
 23. An installation according to claim 21, wherein the means forsubjecting the effluent flow to the solid/liquid separation operationcomprises membrane filtration means.
 24. An installation according toclaim 23, wherein the membrane filtration means is chosen from amongtangential filtration, frontal filtration, and semi-frontal typefiltration means.
 25. An installation according to claim 21, wherein themeans for subjecting the effluent flow to the solid/liquid separationcomprises settlement means.
 26. An installation according to claim 21,wherein the pulsed electric field has characteristics adjusted so thatthe modifying of physicochemical and biological characteristics enableshydrolysis of dissolved substances, aggregation of colloids, complete orpartial destruction of microorganisms, and simultaneous activation ofremaining microorganisms.